LiFePO4 FLAKES FOR Li-ION BATTERY AND METHOD FOR MANUFACTURING THE SAME

ABSTRACT

LiFePO 4  flakes for a Li-ion battery and a method for manufacturing the same are disclosed. The LiFePO 4  flakes of the present invention have a thickness of 5 nm-200 nm, and the angle between the flat surface normal of the flake and the Li-ion diffusion channel is 0°-80°. In addition, according to the present invention, the LiFePO 4  flakes with short Li ion diffusion path can be prepared through a simple process. Hence, not only the charge-discharge efficiency of the Li-ion battery can be improved by use of the LiFePO 4  flakes of the present invention, but also the cost of the Li-ion battery can be further reduced.

CROSS REFERENCE TO RELATED APPLICATION

This application claims the benefits of the Taiwan Patent Application Serial Number 100121791, filed on Jun. 22, 2011, the subject matter of which is incorporated herein by reference.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to LiFePO₄ flakes and a method for manufacturing the same, more particularly, to LiFePO₄ flakes for a Li-ion battery and a method for manufacturing the same.

2. Description of Related Art

As the development of various portable electronic devices continues, more and more attention focuses on the techniques of energy storage, and batteries are the main power supplies for these portable electronic devices. Among commercial batteries, small-sized secondary batteries are especially the major power supplies for portable electronic devices such as cell phones and notebooks. In addition, secondary batteries are applied to not only portable electronic devices, but also electric vehicles.

Among the developed secondary batteries, the lithium secondary batteries (also named as the Li-ion batteries) developed in 1990 are the most popular batteries used nowadays. The cathode material of the initial lithium secondary batteries is LiCoO₂. LiCoO₂ has the properties of high working voltage and stable charging and discharging voltage, so the secondary batteries which use LiCoO₂ as a cathode material are widely applied to portable electronic devices. Then, LiFePO₄ with an olivine structure and LiMn₂O₄ with a spinal structure were also developed as a cathode material for lithium secondary batteries. Compared to LiCoO₂, the safety of the batteries can be improved, the charge/discharge cycles can be increased, and the cost can be further reduced when LiFePO4 or LiMn₂O₄ is used as cathode material of secondary batteries.

Although the batteries which use LiMn₂O₄ as cathode materials have low cost and improved safety, the spinal structure of LiMn₂O₄ may collapse during the deep discharge process, due to Jahn-Teller effect. In this case, the cycle performance of the batteries may further degrade. When LiFePO₄ is used as cathode material of batteries, the batteries also have the properties of low cost and improved safety. In addition, the capacity of LiFePO₄ is higher than that of LiMn₂O₄, so the batteries made from LiFePO₄ can further be applied to devices, which need large current and high power. Furthermore, LiFePO₄ is a non-toxic and environmentally friendly material, and also has great high temperature characteristics. Hence, LiFePO₄ is considered as an excellent cathode material for lithium batteries. Currently, the average discharge voltage of the lithium batteries using LiFePO₄ as a cathode material is 3.4˜3.7 V vs. Li⁺/Li.

A conventional structure of the Li-ion batteries comprises: a cathode, an anode, a separator, and a Li-containing electrolyte. The batteries perform the charge/discharge cycles by the lithium insertion and extraction mechanism, which is represented by the following equations (I) and (II).

Charge: LiFePO₄−x Li⁺−xe³¹ →xFePO₄+(1−x)LiFePO₄   (I)

Discharge: FePO₄+x Li⁺+xe⁻→x LiFePO₄+(1−x)FePO₄   (II)

When a charge process of the batteries is performed, Li ions extract from the structure of LiFePO₄; and the Li ions insert into the structure of FePO₄ when a discharge process is performed. Hence, the charge/discharge process of the Li-ion batteries is a two-phase process of LiFePO₄/FePO₄. However, the diffusion rate of the Li ions in LiFePO₄ and FePO₄ is quite low, so some metal dopants may generally be added into the cathode materials to increase the diffusion rate of the Li ions. In addition, the Li-ion diffusion path of the currently used LiFePO₄ is long, so the conductivity of LiFePO₄ is not good enough. Hence, the LiFePO₄ powders may be coated with carbon to increase the conductivity of LiFePO₄ powders, in order to increase the charge/discharge efficiency of the batteries. However, the process for manufacturing LiFePO₄ powders becomes more complicated when the LiFePO₄ powders are doped with metal additives or coated with carbon. In this case, the cost of the batteries is also increased.

Currently, the LiFePO₄ powders are usually prepared by a solid-state process. However, the property of the product is highly related to the sintering temperature of the solid-state process. When the sintering temperature is below 700° C., all the raw materials have to be mixed well. If the raw materials are not mixed well, Fe³⁺ impurity phase will be present in the LiFePO₄ powders. When sintering temperature is below 600° C., the average grain size of the LiFePO₄ powders will be smaller than 30 μm. However, if the sintering temperature is increased, the average grain size of the LiFePO₄ powders will be larger than 30 μm. When the average grain size of the LiFePO₄ powders is larger than 30 μm, a grinding process and a sieving process have to be performed to obtain powders with grain size between 1 μm to 10 μm. Hence, it is difficult to prepare LiFePO₄ powders with nano-size by the use of the solid-state process.

Therefore, it is desirable to provide a method for manufacturing nano-sized cathode materials of Li-ion batteries in a simple way, in order to increase the charge/discharge efficiency of the batteries and reduce the cost thereof.

SUMMARY OF THE INVENTION

The object of the present invention is to provide LiFePO₄ flakes with a short (Li-ion) diffusion path for use in Li-ion batteries. Hence, the charge/discharge efficiency of the Li-ion battery can further be increased.

Another object of the present invention is to provide a method for manufacturing LiFePO₄ flakes for a Li-ion battery. LiFePO₄ flakes with a short Li-ion diffusion path can be obtained through a simple process by using the method of the present invention, so the cost of the Li-ion batteries can be reduced.

To achieve the object, the present invention provides LiFePO₄ flakes, which have flat shapes, for use in a Li-ion battery. In addition, the thickness of the LiFePO₄ flakes is 5 nm-200 nm, and an angle between a flat surface normal of the LiFePO₄ flakes and a Li-ion diffusion channel is 0°-80°. According to the present invention, the term “normal” means the line, which is perpendicular to the flat surface of the LiFePO₄ flakes.

In addition, the present invention also provides a method for manufacturing the aforementioned LiFePO₄ flakes, which comprises the following steps: (A) providing a mixed organic solution which comprises Li, Fe, and P, wherein the Li contained in the mixed organic solution is derived from a Li-containing precursor or a P and Li-containing precursor, the Fe contained in the mixed organic solution is derived from an Fe-containing precursor or a P and Fe-containing precursor, and the P contained in the mixed solution is derived from a P-containing precursor, a P and Li-containing precursor, or a P and Fe-containing precursor; (B) heating the organic mixed solution to obtain preliminary products; and (C) heat-treating the preliminary products to obtain LiFePO₄ flakes.

According to the LiFePO₄ flakes for the Li-ion battery and the method for manufacturing the same of the present invention, precursors contained in the organic mixed solution are reacted with each other, and then the LiFePO₄ flakes can further be obtained after heat treatment. In addition, the obtained LiFePO₄ flakes of the present invention have an ordered crystal lattice and a short Li-ion diffusion path. The obtained LiFePO₄ flakes of the present invention have flat shapes, even petal-like shapes, so the thickness of the flakes is very thin. Therefore, the insertion and extraction path of the Li ions can be greatly shortened, and the diffusion rate of the Li ions can further be increased. When the obtained LiFePO₄ flakes of the present invention are used as cathode materials of a Li-ion battery, the charge-discharge efficiency of the Li-ion battery can be increased due to the short Li-ion diffusion path. In addition, the efficiency of the Li-ion battery can be improved by using the LiFePO₄ flakes of the present invention without doping any additives or coating any conductive materials, so the cost for manufacturing the Li-ion batteries can be further reduced.

According to the LiFePO₄ flakes for the Li-ion battery of the present invention, an angle between a zone axis of the flat surface of the LiFePO₄ flakes and a b-axis [0, 1, 0] of the Li-ion diffusion channel is 0°-80°, so an angle between a flat surface normal of the LiFePO₄ flakes and a Li-ion diffusion channel is 0°-80°. Preferably, the angle between the zone axis of the flat surface of the LiFePO₄ flakes and the b-axis [0, 1, 0] of the Li-ion diffusion channel is 30°-65°, i.e. the angle between the flat surface normal of the LiFePO₄ flakes and the Li-ion diffusion channel is 30°-65°. More preferably, the angle between the zone axis of the flat surface of the LiFePO₄ flakes and the b-axis [0, 1, 0] of the Li-ion diffusion channel is 45°-60°, i.e. the angle between the flat surface normal of the LiFePO₄ flakes and the Li-ion diffusion channel is 45°-60°.

Preferably, the zone axis of the flat surface of the LiFePO₄ flakes is close to [1,-3, 5].

In addition, according to the LiFePO₄ flakes for the Li-ion battery of the present invention, the width of the LiFePO₄ flakes is not particularly limited. Preferably, the width of the LiFePO₄ flakes is 500 nm-5 μm. More preferably, the width of the LiFePO₄ flakes is 1 μm-2.5 μm.

Furthermore, according to the LiFePO₄ flakes for the Li-ion battery of the present invention, the LiFePO₄ flakes have olivine structures.

According to the method for manufacturing the LiFePO₄ flakes of the present invention, a small amount of metal-containing compounds may be further added in the mixed organic solution in step (A), and the doped metal in the obtained LiFePO₄ flakes can increase the conductivity thereof. Herein, the doped metal can be at least one selected from the group consisting of Mn, Cr, Co, Cu, Ni, V, Mo, Ti, Zn, Zr, Tc, Ru, Rh, Pd, Ag, Cd, Pt, Au, Al, Ga, In, Be, Mg, Ca, Sr, B, and Nb. Preferably, the metal-containing compounds are sulfates, carbonates, nitrates, oxalates, acetates, chlorites, bromides, or iodides of the aforementioned doped metals. More preferably, the metal-containing compounds are sulfates of the aforementioned doped metals. Most preferably, the metal-containing compounds are sulfates of Mn, Cr, Co, Cu, Ni, Zn, Al, or Mg.

Hence, the obtained LiFePO₄ flakes of the present invention are represented by the following formula (I):

LiFe_((1-x))M_(x)PO₄   (I)

wherein, M can be one or more metals selected from the group consisting of Mn, Cr, Co, Cu, Ni, V, Mo, Ti, Zn, Zr, Tc, Ru, Rh, Pd, Ag, Cd, Pt, Au, Al, Ga, In, Be, Mg, Ca, Sr, B, and Nb, and 0≦x<0.5. Preferably, M is one or more metals selected from the group consisting of Mn, Cr, Co, Cu, Ni, Zn, Al, and Mg. More preferably, M is one or more metals selected from the group consisting of Mn, Cu, Zn, Al, Ni, and Mg.

In addition, according to the method for manufacturing the LiFePO₄ flakes of the present invention, a small amount of carbon material may be further added in the mixed organic solution in step (A). In this case, the surfaces of the obtained LiFePO₄ flakes are coated with carbon, so the conductivity of the obtained LiFePO₄ flakes can further be increased. Herein, the carbon materials can be any sugar, such as sucrose. In addition, the additive amount of the carbon material can be 0.1 wt %-20 wt % of the weight of the obtained LiFePO₄ flakes.

According to the method for manufacturing the LiFePO₄ flakes of the present invention, the Li-containing precursor can be at least one selected from the group consisting of LiOH, Li₂CO₃, LiNO₃, CH₃COOLi, Li₂C₂O₄, Li₂SO₄, LiCl, LiBr, and LiI; the Fe-containing precursor can be at least one selected from the group consisting of FeCl₂, FeBr₂, FeI₂, FeSO₄, (NH₄)₂Fe(SO₄)₂, Fe(NO₃)₂, FeC₂O₄, (CH₃COO)₂Fe, and FeCO₃; the P-containing precursor can be at least one selected from the group consisting of H₃PO₄, NaH₂PO₄, Na₂HPO₄, Mg₃(PO₄)₂, and NH₃H₂PO₄; the P and Li-containing precursor can be at least one selected from the group consisting of LiH₂PO₄, Li₂HPO₄, and Li₃PO₄; and the P and Fe-containing precursor can be at least one selected from the group consisting of Fe₃(PO₄)₂, and FePO₄. According to the method for manufacturing the LiFePO₄ flakes of the present invention, the organic mixed solution not only contains the aforementioned precursors, but also may contain other additives such as surfactants, polymer electrolytes, and stabilizers, which can facilitate the synthesis reaction or the dissolution of the precursors. Herein, the examples of the surfactants can be Cetyltrimethylammonium bromide (CTAB), sodium dodecylbenzene sulfonate (SDBS), sodium dodecyl sulfate (SDS), or Triton-X100; the examples of the polymer electrolytes can be polyvinylpyrollidone (PVP), peroxyacetic acid (PAA), Polyethyleneimine (PEI), or polyacrylamide (PAM); and the examples of the stabilizers can be Polyvinyl Alcohol (PVA), or polyvinyl acetate (PVAc). The aforementioned additives can control the crystal size and the preferential growth direction of the powders. In addition, in step (B) of the method of the present invention, an external electric field can be further applied to control the preferential growth direction of the crystal of the powders, in order to increase the area of the Li-ion transfer interface.

According to the method for manufacturing the LiFePO₄ flakes of the present invention, the organic solvent in the mixed organic solution can be any media generally used in the art, and can be any polyol organic solvents generally used in the art. Preferably, the organic solvent is at least one selected from the group consisting of ethylene glycol (EG), diethylene glycol (DEG), glycerol, triethylene glycol (TEG), tetraethylene glycol (TTEG), polyethylene glycol (PEG), Dimethyl sulfoxide (DMSO), and N,N-dimethylmethanamide (DMF). More preferably, the organic solvent used in the method of the present invention is DEG, glycerol, or a combination thereof.

Furthermore, according to the method for manufacturing the LiFePO₄ flakes of the present invention, the organic mixed solution can be reacted through a hydrothermal process, a solvothermal process, a reflux process, or a co-precipitation process, in step (B). Preferably, the organic mixed solution is reacted by reflux. Herein, the reaction temperature of reflux is 105° C.-350° C., and the reaction thereof is 10 hrs-20 hrs, preferably.

In addition, according to the method for manufacturing the LiFePO₄ flakes of the present invention, the organic mixed solution may be heated and reacted under an atmosphere or with an introduced gas flow to obtain the preliminary products in step (B). Herein, the atmosphere or the introduced gas flow can be used as a protective gas or a reducing gas, which may comprise one selected from the group consisting of N₂, H₂, He, Ne, Ar, Kr, Xe, CO, methane, N₂—H₂ mixture, and a mixture thereof. Preferably, the protective gas or the reducing gas is N₂, H₂, or N₂—H₂ mixture. More preferably, the protective gas or the reducing gas is N₂—H₂ mixture.

According to the method for manufacturing the LiFePO₄ flakes of the present invention, the preliminary products may be heat-treated under an atmosphere or with an introduced gas flow to obtain the LiFePO₄ flakes in step (C). Herein, the atmosphere or the introduced gas flow can also be used as a protective gas or a reducing gas, which may comprise one selected from the group consisting of N₂, H₂, He, Ne, Ar, Kr, Xe, CO, methane, N₂—H₂ mixture, and a mixture thereof. Preferably, the protective gas or the reducing gas is N₂, H₂, or N₂—H₂ mixture. More preferably, the protective gas or the reducing gas is N₂—H₂ mixture.

In step (C) of the method for manufacturing the LiFePO₄ flakes of the present invention, the preliminary products are heat-treated at 300° C.-700° C., preferably. In addition, the preliminary products are preferably heat-treated for 1 hr-20 hrs.

In addition, the obtained LiFePO₄ flakes of the present invention can be used as a cathode material to prepare a Li-ion battery, through any conventional method in the art. Here, the method for manufacturing the Li-ion battery is briefly described, but the present invention is not limited thereto.

An anode current collector is coated with a carbon material, and then the carbon material is dried and pressed to form an anode for the Li-ion battery. A cathode current collector is coated with a cathode active material (i.e. the LiFePO₄ of the present invention), and then the cathode active material is dried and pressed to form a cathode for the Li-ion battery. Next, a separator is inserted between the cathode and the anode, a Li-containing electrolyte is injected, and a Li-ion battery is obtained after packaging.

Other objects, advantages, and novel features of the invention will become more apparent from the following detailed description when taken in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG 1A is an XRD diffraction pattern of preliminary products before heat-treating process according to Embodiment 1 of the present invention;

FIG. 1B is an XRD diffraction pattern of LiFePO₄ flakes according to Embodiment 1 of the present invention;

FIGS. 2A and 2B are SEM photos of LiFePO₄ flakes according to Embodiment 1 of the present invention;

FIG. 3 is a schematic drawing of the Li ion diffusion path of LiFePO₄ flakes according to Embodiment 1 of the present invention; and

FIG. 4 is SEM photo of LiFePO₄ flakes according to Embodiment 3 of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

The present invention has been described in an illustrative manner, and it is to be understood that the terminology used is intended to be in the nature of description rather than of limitation. Many modifications and variations of the present invention are possible in light of the above teachings. Therefore, it is to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described.

Embodiment 1

The precursors of H₃PO₄, FeC₂O₄, and LiOH were mixed in a ratio of 1:1:1, and dissolved in DEG (300 ml) to obtain a mixed organic solution (0.15 M). Next, the mixed organic solution was reacted by reflux at 200° C., under an atmosphere of N₂—H₂ mixture for 18 hrs. After the mixed organic solution was filtrated, preliminary products were obtained. Then, the preliminary products were heat-treated at 500° C., under an atmosphere of N₂ gas for 2 hrs to obtain LiFePO₄ flakes of the present embodiment.

The preliminary products before heat-treatment of the present embodiment were examined by an X-ray diffractometer (Shimadzu 6000) to obtain the crystal structure thereof. The X-ray diffraction pattern was obtained by applying Cu Kα radiation, the 2θ-scanning angle is 15°-45°, and the scanning rate is 1°/min. The obtained XRD diffraction patterns are shown in FIGS. 1A and 1B, wherein FIG. 1A is an XRD diffraction pattern of preliminary products before heat-treatment, and FIG. 1B is an XRD diffraction pattern of LiFePO₄ flakes.

According to FIGS. 1A and 1B, the upper figures are the XRD diffraction patterns of the preliminary products and the LiFePO₄ flakes of the present embodiment, and the lower figures are the XRD diffraction patterns of LiFePO₄ crystal with an olivine structure (JCPDS No. 81-1173). As shown in the upper figures of FIGS. 1A and 1B, lines are used to indicate the position of the peaks.

As shown in FIG. 1A, the preliminary products before heat-treatment do not have olivine structures. On the contrary, as shown in FIG. 1B, the lines indicating the peaks of the LiFePO₄ flakes of the present embodiment correspond to the peaks of LiFePO₄ crystal with the olivine structure (JCPDS No. 81-1173), and there are no other peaks observed in the LiFePO₄ flakes of the present embodiment. This result indicates that all the LiFePO₄ flakes of the present embodiment are LiFePO₄ flakes with olivine structures.

In addition, the shapes of the LiFePO₄ flakes of the present embodiment were observed with a scanning electron microscope (SEM) (Hitachi S-4000), and the results are shown in FIGS. 2A and 2B. As shown in FIG. 2A, the LiFePO₄ flakes have flat shapes (also named as petal-like shapes), and the width of each flake is 2 μm, when the LiFePO₄ flakes were observed at the magnification of 100000×. As shown in FIG. 2B, when the LiFePO₄ flakes were observed at the magnification of 600000×, it can be observed that the thickness of each flake is 50 nm, and the width of the surface of each flake is 40 folds of the thickness of each flake.

Furthermore, a transmission electron microscope (TEM) (JEOL 2010) was used to observe the single-crystal diffraction of the powders. The result shows that the zone axis of the LiFePO₄ flakes of the present embodiment is close to [1, −3, 5], and the angle between the zone axis [1, −3, 5] and the surface normal of each diffraction planes is in a range from 89.33° to 90.33°. After calculation, the angle between the zone axis [1, −3, 5] and a b-axis [0, 1, 0] of the Li-ion diffusion channel is 54.93°, which is obtained by the following equations:

[1, −3, 5] ⋅ [0, 1, 0] = [1, −3, 5] × [0, 1, 0] × cos  θ ${\cos \; \theta} = {\frac{{- 3}b^{2}}{\sqrt{a^{2} + {9b^{2}} + {25c^{2}}} \times \sqrt{b^{2}}} = {- 0.5753}}$

wherein, a is 10.33 Å, b is 6.01 Å, c is 4.692 Å, and a, b and c are respectively the length of the unit vector along the x, y and z crystal axes of the LiFePO₄ flakes. After calculation, θ is 125.07°, which can be taken into) 54.93° (180°-125.07°=54.93°.

In other words, as shown in FIG. 3, the angle α between the Li-ion diffusion channel and the normal of the surface 101 of the flake of the LiFePO₄ flakes 10 of the present embodiment is 54.93°. The longest diffusion path x for the Li-ion to leave the LiFePO₄ flakes with the thickness D of 50 nm is (50 nm/(2× cos 54.93°)=43.5 nm

Embodiment 2

The precursors of H₃PO₄, FeSO₄, and Li₂CO₃ (1:1:1) and urea with the same molar amount were dissolved in DEG (300 ml) to obtain a mixed organic solution (0.3 M). Next, the mixed organic solution was reacted by reflux at 200° C., under an atmosphere of N₂—H₂ mixture for 14 hrs. After the mixed organic solution was filtrated, preliminary products were obtained. Then, the preliminary products were heat-treated at 500° C., under an atmosphere of N₂ gas for 10 hrs to obtain LiFePO₄ flakes of the present embodiment.

The LiFePO₄ flakes of the present embodiment were examined with an X-ray diffractometer, a scanning electron microscope, and a transmission electron microscope by the same methods as disclosed in Embodiment 1. The result of the X-ray diffraction shows that the LiFePO₄ flakes of the present embodiment have olivine structures. The result of SEM shows that the LiFePO₄ flakes of the present embodiment have flat shapes, the width of each flake is 1-1.5 μm, the thickness thereof is 20-35 nm, and the width of the surface is 43-50 folds of the thickness thereof.

In addition, the result of TEM shows that the angle between the zone axis and the surface normal of each diffraction planes of the LiFePO₄ flakes of the present embodiment is in a range from 89.33° to 90.33°. The angle between the zone axis [1, −3, 5] and the b-axis [0, 1, 0] of the Li-ion diffusion channel is calculated to be 54°.

Embodiment 3

The precursors of H₃PO₄, FeC₂O₄, and LiOH were mixed with a ratio of 1:1:1, and dissolved in DEG (300 ml) to obtain a mixed organic solution (0.15 M). Next, SDS was added into the mixed organic solution, and the mixed organic solution was reacted by reflux at 200° C., under an atmosphere of N₂ gas for 10 hrs. After the mixed organic solution was filtrated, preliminary products were obtained. Then, the preliminary products were heat-treated at 500° C., under an atmosphere of N₂ gas for 4 hrs to obtain LiFePO₄ flakes of the present embodiment.

The shapes of the LiFePO₄ flakes of the present embodiment were observed with a scanning electron microscope (SEM). As shown in FIG. 4, the LiFePO₄ flakes have flat shapes (also named as petal-like shape) and bundle like a rose, and the thickness of each flake is thin and uniform, when the LiFePO₄ flakes were observed at the magnification of 100000×. In addition, the SEM result also shows that the dispersion of the LiFePO₄ flakes of the present embodiment is better than that of Embodiment 1.

According to the results of Embodiments 1 to 3, the LiFePO₄ flakes of the present invention have unique shapes, so the distribution density of the Li-ion diffusion channel is the highest. In addition, the LiFePO₄ flakes of the present invention are flakes, so Li ions can extract from the powders in a uniform and high-density manner. Therefore, the current density of the Li-ion batteries can be further increased by the use of the LiFePO₄ flakes of the present invention.

Furthermore, the length of the Li-ion diffusion channel is similar to the thickness of the LiFePO₄ flakes of the present invention, so Li ions can quickly diffuse inside the powders. Even though there are no metal additives doped into the LiFePO₄ flakes of the present invention, the high diffusion rate of the Li ions can still be maintained. In addition, the number of Li ions extracting from the powders is not significantly reduced over time, so an almost constant charge/discharge current can be obtained. Therefore, even if the charge/discharge time is increased, the problem of the reduction of charge/discharge current can be prevented by the use of the LiFePO₄ flakes of the present invention.

In addition, the length of the Li-ion diffusion channel according to the LiFePO₄ flakes of the present invention is in nano scale, so the problem of low conductivity can be avoided. Hence, when the LiFePO₄ flakes of the present invention are applied to Li-ion batteries, cathode materials with high conductivity can be obtained without carbon coating.

In conclusion, according to the LiFePO₄ flakes and the method for manufacturing the same of the present invention, the thickness of the obtained LiFePO₄ flakes is only of nano scale. Even though there are no metal additives doped into the LiFePO₄ flakes or no carbon coated on the surface of the LiFePO₄ flakes, the charge/discharge character of the batteries can still be improved. In addition, the process of the method for manufacturing the LiFePO₄ flakes of the present invention is simple. Therefore, when the LiFePO₄ flakes of the present invention are applied to Li-ion batteries, the cost thereof can be further decreased.

Although the present invention has been explained by its preferred embodiment, it is to be understood that many other possible modifications and variations can be made without departing from the spirit and scope of the invention as hereinafter claimed. 

1. LiFePO₄ flakes for a Li-ion battery, wherein the thickness of the flakes is 5 nm-200 nm, and an angle between a surface normal of the LiFePO₄ flakes and a Li-ion diffusion channel is 0°-80°.
 2. The LiFePO₄ flakes as claimed in claim 1, wherein the LiFePO₄ flakes have petal-like shapes.
 3. The LiFePO₄ flakes as claimed in claim 1, wherein the angle between the flat surface normal of the LiFePO₄ flakes and the Li-ion diffusion channel is 30°-65°.
 4. The LiFePO₄ flakes as claimed in claim 1, wherein an angle between a zone axis of the flat surface of the LiFePO₄ flakes and a b-axis [0, 1, 0] of the Li-ion diffusion channel is 0°-80°.
 5. The LiFePO₄ flakes as claimed in claim 4, wherein the angle between the zone axis of the surface of the LiFePO₄ flakes and the b-axis [0, 1, 0] of the Li-ion diffusion channel is 30°-65°.
 6. The LiFePO₄ flakes as claimed in claim 1, wherein a width of the LiFePO₄ flakes is 500 nm-5 μm.
 7. The LiFePO₄ flakes as claimed in claim 1, wherein the LiFePO₄ flakes have olivine structures.
 8. A method for manufacturing LiFePO₄ flakes for a Li-ion battery, comprising the following steps: (A) providing a mixed organic solution, which comprises Li, Fe, and P, wherein the Li contained in the mixed organic solution is derived from a Li-containing precursor or a P and Li-containing precursor, the Fe contained in the mixed organic solution is derived from an Fe-containing precursor or a P and Fe-containing precursor, and the P contained in the mixed solution is derived from a P-containing precursor, a P and Li-containing precursor, or a P and Fe-containing precursor; (B) heating the organic mixed solution to obtain preliminary products; and (C) heat-treating the preliminary products to obtain LiFePO₄ flakes.
 9. The method as claimed in claim 8, wherein the organic mixed solution is heated under an atmosphere or with an introduced gas flow to obtain the preliminary products, in step (B).
 10. The method as claimed in claim 8, wherein the preliminary products are heat-treated under an atmosphere or with an introduced gas flow to obtain the LiFePO₄ flakes, in step (C).
 11. The method as claimed in claim 8, wherein the Li-containing precursor is at least one selected from the group consisting of LiOH, Li₂CO₃, LiNO₃, CH₃COOLi, Li₂C₂O₄, Li₂SO₄, LiCl, LiBr, and LiI.
 12. The method as claimed in claim 8, wherein the Fe-containing precursor is at least one selected from the group consisting of FeCl₂, FeBr₂, FeI₂, FeSO₄, (NH₄)₂Fe(SO₄)₂, Fe(NO₃)₂, FeC₂O₄, (CH₃COO)₂Fe, and FeCO₃.
 13. The method as claimed in claim 8, wherein the P-containing precursor is at least one selected from the group consisting of H₃PO₄, NaH₂PO₄, Na₂HPO₄, Mg₃(PO₄)₂, and NH₃H₂PO₄.
 14. The method as claimed in claim 8, wherein the P and Li-containing precursor is at least one selected from the group consisting of LiH₂PO₄, Li₂HPO₄, and Li₃PO₄.
 15. The method as claimed in claim 8, wherein the P and Fe-containing precursor is at least one selected from the group consisting of Fe₃(PO₄)₂, and FePO₄.
 16. The method as claimed in claim 8, wherein the mixed organic solution further comprises: at least one selected from the group consisting of a surfactant, a polymer electrolyte, and a stabilizer.
 17. The method as claimed in claim 8, wherein an organic solvent in the mixed organic solution is at least one selected from the group consisting of ethylene glycol (EG), diethylene glycol (DEG), glycerol, triethylene glycol (TEG), tetraethylene glycol (TTEG), polyethylene glycol (PEG), Dimethyl sulfoxide (DMSO), and N,N-dimethylmethanamide (DMF).
 18. The method as claimed in claim 9, wherein the atmosphere or the introduced gas flow comprises one selected from the group consisting of N₂, He, Ne, Ar, Kr, Xe, CO, methane, N₂—H₂ mixed gas, and a mixture thereof.
 19. The method as claimed in claim 10, wherein the atmosphere or the introduced gas flow comprises one selected from the group consisting of N₂, He, Ne, Ar, Kr, Xe, CO, methane, N₂—H₂ mixed gas, and a mixture thereof.
 20. The method as claimed in claim 16, wherein the surfactant is Cetyltrimethylammonium bromide (CTAB), sodium dodecylbenzene sulfonate (SDBS), sodium dodecyl sulfate (SDS), or Triton-X100.
 21. The method as claimed in claim 16, wherein the polymer electrolyte is polyvinylpyrollidone (PVP), peroxyacetic acid (PAA), Polyethyleneimine (PEI), or polyacrylamide (PAM).
 22. The method as claimed in claim 16, wherein the stabilizer is Polyvinyl Alcohol (PVA), or polyvinyl acetate (PVAc).
 23. The method as claimed in claim 8, wherein the organic mixed solution is heated to and reacted at 105°-350° C., in step (B).
 24. The method as claimed in claim 8, wherein the organic mixed solution is reacted for 10 hrs-20 hrs.
 25. The method as claimed in claim 8, wherein the preliminary products are heat-treated at 300°-700° C., in step (C).
 26. The method as claimed in claim 8, wherein the preliminary products are heat-treated for 1 hr-20 hrs.
 27. The method as claimed in claim 8, wherein the LiFePO₄ flakes have a thickness of 5 nm-200 nm, and an angle between a flat surface normal of the LiFePO₄ flakes and a Li-ion diffusion channel is 0°-80°.
 28. The method as claimed in claim 8, wherein the LiFePO₄ flakes have olivine structures. 